Method of producing an ortho-directed
phenolic resin by condensing phenol
and hcho in the presence of a bivalent
metal ion and then adding resorcinol,
and the resultant product



United States Patent Int. Cl. C08g 5/10 US. Cl. 260-52 7 Claims Matter enclosed in heavy brackets appears in the original patent but forms no part of this reissue specification; matter printed in italics indicates the additions made by reissue.

ABSTRACT OF THE DISCLOSURE A process of manufacturing ortho-directed, phenolformaldehyde resins, modified with resorcinol or other polyhydroxy aromatic compounds which have a relatively long shelf life and relatively short cure time by condensing phenol and formaldehyde to near completion under reflux conditions in the presence of bivalent metal ion catalyst, adding resorcinol or other polyhydroxy aromatic compounds to the reaction product of phenol and formaldehyde, and continuing heating of the mixture under reflux condition until the reaction is substantially complete. The molecular ratio of phenol to formaldehyde is between 0.55 to 1.2 moles formaldehyde per mole of phenol and the molecular ratio of resorcinol or other polyhydroxy aromatic compound to phenol ranges be tween 0.2 to 0.8 moles.

The final copolymer has a predominantly linear backbone of ortho-directed phenol-formaldehyde modified by resorcinol or other polyhydroxy aromatic compound forming methylene bridges cross-linking molecules to adjacent molecules to provide an infusible final product.

This invention relates to the production of a resin produced by reacting an aldehyde with a phenol in the presence of a particular catalyst and further reacting the combined phenol-aldehyde mass with polyhydroxy aromatics. More specifically, this invention relates to the production of a phenol-formaldehyde resorcinol resin in the presence of an ortho-directing catalyst.

In the manufacture of laminated wood products, it is the usual practice to spread an adhesive between at least two wooden laminates and then press them together at either ambient or elevated temperatures.

In recent years the forest product industry has developed highly sophisticated machinery for rapidly moving laminates together with adhesive therebetween for bonding. However, in order to effectively bond the laminates together, it is required that they remain in the press a predetermined period of time. Therefore, the rate of production is dependent on the length of time the laminates need to be in the press.

The adhesives used in these systems are usually formed from a phenol formaldehyde resin having conventional additives mixed therewith. The phenol and formaldehyde are combined by cooking a predetermined amount of each component together in the presence of an alkaline catalyst. The end product is a resin polymer that will cure to a hard infusible state when subjected to heat. While these resins form a good bond between a pair of laminates,

"ice

they generally require long press times at high temperatures.

In order to reduce the long press time when using a phenol-formaldehyde resin, it has been proposed to modify this resin with a resorcinol-aldehyde reaction product. However, in practice it has been found that press times are not appreciably reduced by this type of resin.

Also, it has been proposed to add resorcinol to the combined phenol-formaldehyde polymer to shorten press time for complete cure. However, this expedient seriously reduces the pot life of the resin product which requires immediate use of the resin; but, most production lines require storage of the resin to ensure an adequate supply. Thus, this type of resin has been proven to be unsatisfactory.

The object of this invention is to provide a method of producing a phenol aldehyde resin modified with a polyhydroxy aromatic compound that has a relatively long shelf life and a relatively short cure time at ambient or moderately elevated temperatures.

Another object of this invention is to provide a resin [product] produced by reacting an aldehyde with phenol in the presence of an ortho-directing catalyst and further modified with resorcinol to provide the resin with a relatively long shelf life and a relatively short cure time.

In the practice of the present invention, phenol and formaldehyde are mixed together in a cooking vessel of any desired size in the presence of an ortho-directing catalyst. A catalyst suitable for use with the present invention is a bivalent metal ion such as calcium, magnesium, zinc, strontium, cadmium, or barium. In use, the catalysts are usually bivalent metal salts of Weak organic acids that are soluble in the phenol-formaldehyde mixture. Typical are the acetate, citrate, glycolate, and tartrate salts.

During the initial cooking stage of formulating the resin, a particular amount of formaldehyde is used with the phenol. It has been found that a molecular ratio of from 0.55 to 1.2 moles of formaldehyde per mole of phenol is suitable. The pH of this reaction mass will be about 6. The phenol formaldehyde mass is cooked at reflux temperature in the presence of the bivalent metal catalyst until the reaction is near completion. By the term near completion it is meant that the viscosity of the reaction mass is about centipoise at 25 C. with a solid content of up to 65%. The formaldehyde will attach predominately at the ortho position to provide the following typical polymer:

wherein n is preferably a number greater than 1 and will depend on the molar ratio of the phenol and formaldehyde.

The temperature of the phenol formaldehyde reaction mass is now slightly reduced below reflux temperature and resorcinol is added. The amount of resorcinol added may range from between 0.2 to 0.8 mole of resorcinol per mole of phenol. By adding the resorcinol to the reaction mass, the temperature thereof will be further reduced. This initial reduction of temperature will allow the intermixing of the resorcinol throughout the phenol formaldehyde reaction mass before substantial reaction takes place. The temperature of the phenol formaldehyde resorcinol mass is then raised back up to reflux temperature of approximately 96 to 98 C. After the phenol resorcinol formaldeyhde mass has been reheated, an alkali metal CHaOH hydroxide, water and an alcohol may be added. The function of the alcohol is to prevent phase separation of the resin during storage. The function of the alkali metal hydroxide is to stabilize, catalyze and wet and may be used in an amount ranging up to about 11% by weight.

The resorcinol phenol formaldehyde mass is then cooked until the viscosity is between 620 and 1300 centipoise. The time necessary to complete the cook is about hrs. In order to increase the reaction rate between the phenol formaldehyde and resorcinol, the whole mass may be placed under pressure. This expedient will necessarily increase the reflux temperature and a faster reaction rate will occur. After the mass has reacted to the degree as set forth, the reaction mass is then cooled and shipped to the mill to be further processed and used. The resin mass to be shipped to the mill will have a storage life of about 30 days and will contain at least 50% solids. The resin product will have the following typical formula:

wherein n is preferably a number greater than 1 and will depend on the molar ratio of the phenol and formaldehyde.

When it is desired to formulate a thermosetting adhesive from the above resin, it is required that a hardener be 0H 0H OH H f --CH CH i l mixed therewith. It has been found in practice that commercial powdered hardeners consisting of a mixture of paraformaldehyde and fillers cannot be suitably employed with the resin of this invention. Such hardeners have the possibility of caking or lumping under humid conditions and require long and complicated mixing requirements to blend the lightweight powders with the liquid resin. Accordingly, a novel type liquid hardener was formulated.

The process for formulating the hardner is to mix to 50 parts of water, up to 30 parts of an alcohol and 10 to 70 parts of formaldehyde solution in a vessel and stir continuously for a sufiicient length of time to fully intermix these ingredients. Thereafter, a dry blend of between and 40 parts filler and up to 2 parts hydroxyethyl cellulose is mixed in with the water, alcohol and formaldehyde. This mixture is blended until the dry ingredients are thoroughly intermixed therein. Then up to 5 parts of pyrogenic silica is added to the mixture and thoroughly mixed until a smooth paste is formed. Then up to [13] 80 parts of formaldehyde solution is added to the mass along with up to 2 parts of a wetting agent and the whole mass is then thoroughly mixed. After the mass is thoroughly mixed, it is strained into a shipping container and stored. The mixture is thixotropic and does not readily settle out. After long periods of standing, a shallow, clear liquid layer may form on top but can be readily mixed in. The product is a thick, milky liquid.

As can be seen, the hardener consists of a liquid mixture of filler and aldehyde. Suitable fillers can be various clays, silica flour prepared from crystalline or amorphous silica, nutshell flours, chalk flour, powdered asbestos and bark and wood flours. Of these, aluminum silicate clay, walnut shell flour, and crystalline silica flour have been found to have the most desirable properties. Combinations of these fillers may be used suitably. Of the aldehydes, it has been found that aqueous paraformaldehyde dispersions, various formalin solutions, glyoxal and furfuralaldehyde alone or in combinations are suitable. However, any

aldehyde with enough activity to harden the phenol resorcinol polymer at room or intermediate temperature is suitable. The other ingredients serve as modifiers and stabilizers. Alcohol stabilizes formalin solutions against precipitation and gelation. The pyrogenic silica helps prevent separation of the hardener dispersion and imparts thixotropy to the hardener and to the mixed glue. The hydroxyethyl cellulose and the wetting agent aid in dispersing the solid ingredient of the hardener and prevent separation. The hydroxyethyl cellulose also serves as a protective colloid for the dispersion.

The above hardener is mixed with the resin mass at a ratio of from 1 to 5 parts of resin per 1 part of hardener. After the hardener has been thoroughly mixed with the resin, the resin begins to react and now has a very short pot life. Accordingly, it is desirable that the resin and hardener be continuously mixed together and continuously applied to the wood to be bonded together. The continuous mixing and metering may be done by any commercial mixer capable of mixing two liquids together at a predetermined ratio.

The adhesive that is applied to the wood to be bonded together will have a viscosity of preferably between 600 and 8000 centipoise to provide the requisite spreadability properties thereof. The molecular ratio of the resorcinol to phenol will be between .2 to .8 mole of resorcinol per mole of phenol with the molecular ratio of formaldehyde to total phenolics of 0.70 to 2.0. The final adhesive product will have the following typical formula:

wherein n is preferably a number greater than 1 and will depend on the molar ratio of the phenol and formaldehyde. It is apparent from this formula that methylene bridges have been formed, crosslinking the molecule to adjacent molecules, to provide the infusible final product.

As has been pointed out above, the resin will be at least 50% solids by weight. However, for some particular types of bonding procedures, it is not necessary to provide such a high solids content of the resin. Accordingly, the resin may be diluted by adding water thereto in a particular manner. The mere expedient of adding additional water will not result in a satisfactory resin.

Accordingly, when a resin is formulated having less solids therein, it is necessary to add water with the resorcinol when it is added to the reaction mass of the phenol and formaldehyde. The amount of water will be dictated in accordance with the amount of solids that are required in the final product. Ordinarily, sufficient water can be added to produce a resin having a final solids content of 35% based on the weight of the final resin. This resin can then be mixed with the hardener and formulated as set forth above for the final resin adhesive product. This resin will have the same molecular ratio and approximately the same viscosity as the resin noted above only with fewer solids based on the weight percent.

The above resin has found wide acceptance in the laminating industry because of the durability and cold setting nature of the resorcinol phenol formaldehyde resins. Particular acceptance has been found when laminating exterior beams. In other applications, the resorcinol phenol formaldehyde resins are advantageous because of their cold setting and rapid heat curing features and the durable nature of the resin after cure. The chief limitation, however, of these resins is their high cost due to the expense in obtaining resorcinol. Accordingly, the wood laminating companies and their suppliers have put forth a great deal of effort to try to replace the resorcinol portion of the resins.

In accordance with another feature of this invention,- it has been found that a low cost polyhydric aromatic compound can be substituted for the resorcinol in the above resins. Tests show that such a substitution in conyentional resin formulations results in a resin that is clearly unsatisfactory for most resin uses. These polyhydric aro matics are polyhydric, polynuclear aromatics and may also include one or more of the dihydroxy benzenes. The above materials may be prepared by reacting monochlorophenols with alkali metal hydroxides in accordance with Belgian Pat. N0. 663,903. filed May 13, 1965, and issued to Dow Chemical Company of Midland, Mich. While the compositions per se above noted form no part of the present invention, it has been found that these materials may be substituted for the resorcinol content in the resin formulations as herein defined. Accordingly, for a complete disclosure of the process for formulating the above compositions and the description of the compositions per se, reference is made to the above-noted Belgian patent.

In order to illustrate the merits of the present invention, reference is made to the following examples:

Example I A resin was formulated by mixing together 45.48 parts by weight of 90% phenol (90% phenol and water), 11.11 parts by weight 91% paraformaldehyde, 4.37 parts by weight water, and 0.44 part by weight calcium acetate in a cooking vessel which was heated to reflux temperature of 106 C. uniformly in 60 min. The temperature of the materials in the cooking vessel was held at the reflux temperature for 135 min. and then was slightly cooled. It was found that the phenol and formaldehyde had combined and had a viscosity of 125 centipoise at 25 C., a pH of 6, and an oven solids content of 60.1 parts by weight. Thereafter, 19.19 parts by weight resorcinol was added to the phenol formaldehyde reaction mass and heated back to reflux in min. Then 6.55 parts by weight water, 9.59 parts by weight ethanol, and 3.27 parts by weight of a 50% solution of sodium hydroxide were added to the reaction vessel. The entire mass was then cooked at reflux temperature between 96 and 98 C. until the reaction mass reached a viscosity of between 880 and 1070 centipoise measured at 25 C. The mass was then cooled to room temperature and stored.

6 Example 111 A liquid hardener was formulated by placing in a vessel 32.40 parts by weight water, 3 parts by weight methanol, and 30.00 parts by weight of 46.5% formalin. This mixture of materials was stirred continuously. A dry blend of 25 parts by weight ASP-400 clay filler and .12 hydroxyethyl cellulose was prepared. This dry blend was added to the vessel and stirred in while 4.40 parts by weight Cab-O-Sil M5, pyrogenic silica, was added. A smooth paste was achieved. Then 5 parts by weight 46.5% formalin was added along with .10 part by weight Advawet 43, wetting agent. This mixture of materials was mixed thoroughly and then strained into a shipping container through a 30-mesh screen and stored. The viscosity of this material measured on a Brookfield viscometer with a No. 4 spindle was as follows: at 6 r.p.m., viscosity 10,000 centipoise; at 12 r.p.m., 6000 centipoise; at 30 r.p.m., 2940 centipoise.

Example IV The resin of Example I and liquid hardener of Example III were mixed together at a ratio of 5 parts of resin to 2 parts of hardener in a continuous manner and then applied to Douglas fir boards and laminated into beams. Tests were performed on the laminated beams using CS253-63 procedures with the following results:

A series of resins was made in accordance with the formulation as set out in Example I but varying the amount of resorcinol used with the amounts of the other constituents being held constant. Each of the resins was admixed with the liquid hardener of Example HI at a ratio of 5 parts resin to 2 parts liquid hardener. Tests on this adhesive mix were as follows:

TABLE II Resin number 1161-44 116143 1115-101 111598 113L 1161-45 1161-46 116147 1161-48 Resorcinol: Phenol molar ratio...-- 0. 0. 0. 0. 0. 0. 50 0. 0. 0. 100 C. gel time, min 57 62 104 157 846 2, 485 2, 980 1,714 1, 746 Tests on adhesive mix (5 parts resin, 2 parts liquid hardener), block shear 3 values for 11 hr. clamp time:

Strength, p.s.l l, 003 1, 103 841 1, 127 1, 220 1,162 1, 051 1, 163 1, 300 Percent wood failure 78 47 100 98 87 87 100 38 Percent delamlnation 0 0 0 0 0 0 0 0 0 1 The 100 C. gel time is a measure of storage life.

3 The block shear results were determined by the AIIC procedure and involved 70#/M ft. spread and 10 min. open assembly time.

Example II A second resin formulation was made by placing in a cooking vessel 28.89 parts by weight 90% phenol (90% phenol and 10% water), 7.57 parts by weight 91% paraformaldehyde, 3.31 parts by weight water, and 0.28 part by weight calcium acetate. The ingredients were heated to reflux at 106 C. uniformly in 60 min. The mass was held at the reflux temperature for an additional min. and then slightly cooled. Then 12.39 parts by weight resorcinol was added to the phenol formaldehyde reaction mass and heated back to reflux in 15 min. Then 16.89 parts by weight water and 2.12 parts by weight of a 50% solution of sodium hydroxide was added. This mass was then cooked at reflux to a viscosity of 3620 centipoise measured at 25 C. Then 22.35 parts by weight water and 6.20 parts by weight ethylene glycol was added and cooked until the mass had a viscosity of 627 centipoise measured at 25 C. The resin was then cooled to room temperature and stored.

Example VI Example VII The resin of Example I was formulated but modified by substituting a mixture of polyhydric aromatic compounds for the resorcinol content on a weight basis. An adhesive was formulated from this resin by adding thereto a liquid hardener in accordance with Example III at a 7 8 ratio of parts resin to 2 parts hardener. The adhesive bivalent metal ion catalyst, the molecular ratio of was placed on boards which were laminated together. A formaldehyde to phenol being between 0.55 to 1.2 conventional phenol formaldehyde resorcinol resin was moles formaldehyde per mole of phenol, again formulated except a mixture of polyhydric aromatic (2) adding a mixture of polyhydroxy aromatics includmaterials was substituted for the resorcinol content. The ing dihydn'c-phenols, polyhydroxy-[polyphenal] conventional resin was formulated in the conventional polyphenyl ethers and polyhydroxy-polyphenyls manner using a sodium hydroxide catalyst. Block shear formed by the reaction of at least three moles of an tests for the two resins were then performed using a 7 alkali metal hydroxide with a chlorophenate at a hour clamp time at 22 C. and 150 p.s.i. with the result temperature of from 200 C. to about 350 C., While that the resin of Example I, but modified by employing a m maintaining the reaction product of formaldehyde mixture of polyhydric aromatic compounds for the resand phenol atanelcvated temperature, and orcinol content, had a shear strength of 880 p.s.i. at 7 (3) heating the reaction mass under reflux conditions hours clamp time while the conventional catalyzed resin until the viscosity is between 620 and 3000 centihad a shear strength of 260 p.s.i. poises.

From the above examples and tables, it is clear that 5 6. Aresin having predominantly the structure:

3;; ii i QW the resin and adhesive of this invention exhibit bonding wherein the molecular ratio of resorcinol to phenol ranges properties and shelf life in quantities far superior to those from 0.2 to 0.8 moles resorcinol per mole phenol, the of a conventional phenol formaldehyde resorcinol resin. molecular ratio of formaldehyde to total phenolics ranges While specific details of preferred embodiments have from [0.70] 0.30 to [2.0] 1.0 moles formaldehyde per been set forth above, it will be apparent that many mole total phenolics, n is greater than 1, and the viscosity changes and modifications may be made therein without ranges between [600] 620 and [8000] 3000 centipoises. departing from the spirit of the invention. It will, there- 7. The process according to claim 1 wherein formfore, be understood that what has been described herein 4" aldehyde and phenol are reacted together to a viscosity is intended to be illustrative only, and is not intended to of about 125 centipoises at C. limit the scope of the invention.

What is claimed is: References Cited 1. A process for the manufacture of a resin composi- The f ll i references, cited by the Examiner, are U011. P the Steps 051 of record in the patented file of this patent or the original (1) reacting formaldehyde and phenol to near complepatent.

tion under reflux conditions in the presence of a bi- UNITED STATES PATENTS valent metal ion catalyst, the molecular ratio of formaldehyde to phenol being between 0.55 to 12 moles :23:3 fomlaldehyde p mole of phenol! R odes (2) adding resorcinol to the reaction product in a mo 2639258 5/1953 E "15km lecular ratio of 0.2 to 0.8 [mole resorcinal] mole 18 2/1956 J13: e a 2? resorcinol per mole of phenol while maintaining the 2940954 6/1960 B e reaction mass at elevated reaction temperature, and 1851021 3,1932 2 9 (3) heating the resin mixture under reflux conditions 2489336 11/1949 e i E until 'the viscosity is between 620 and 3000 centi- Pahr et a 54 poises. th 1 h h OTHER REFERENCES 2. A process in accordance wi c aim 1 w erein t e catalyst is a bivalent metal salt of a weak organic acid. ggzg f Resms Chemlstry Megson 1958 pages 171 3. A process in accordance with claim 2 wherein the Ch of o l 7 bivalent metal ion catalyst may be selected from the pp 5 3 C mmerclal P asucs Wakema'n 194 group consisting of calcium acetate, magnesium acetate, zinc acetate, strontium acetate, cadmium acetate, barium Modem Hashes Encyclopedla 1961 M1228 acetate ormimres thmof- WILLIAM H. SHORT, Primary Examiner 4. A process in accordance with claim 3 wherein the bivalent metal ion catalyst is calcium acetate. SCHAIN Asslstant Bummer 5. A process for the manufacture of a resin composi- U S CI x3 tion, comprising the steps of:

(1) reacting formaldehyde and phenol to near comple- 161-262; 260-14, 17.2, 29.3, 30.4, 33.4, 45.95, 54, 57

tion under reflux conditions in the presence of a 79 Disclaimer Reissue N0. 26,881.-R0lmzcl E. Kreibich, Harlan G. F ream/m, and G'e'ne F. Baxter, Seattle, VVash., and Karl F. Kumli. Chico, Calif. METHOD OF PRODUCING AN ORTHO'DIRECTEI) PHENOLIC RES- IN BY CONDENSING PHENOL AND HCIIO IN THE PRES- ENCE OF A BIVALENT METAL ION AND THEN ADDING RESORCINOL, AND THE RESULTANT PRODUCT, Patent dated May 19, 1970. Disclaimer filed July 29, 1971, by the assignee, Weyerhaeusev' (lampuny.

Hereby enters this disclaimer to claims 1-7 of said patent.

[Official Gazette Normnbei" 9, 7977.] 

